Abstract
In this paper a 600 MW oxy-type coal unit with a pulverized bed boiler and a membrane-cryogenic oxygen separator and carbon capture installation was analyzed. A membrane-cryogenic oxygen separation installation consists of a membrane module and two cryogenic distillation columns. In this system oxygen is produced with the purity equal to 95%. Installation of carbon capture was based on the physical separation method and allows to reduce the CO2 emission by 90%. In this work the influence of the main parameter of the membrane process-the selectivity coefficient, on the efficiency of the coal unit was presented. The economic analysis with the use of the break-even point method was carried out. The economic calculations were realized in view of the break-even price of electricity depending on a coal unit availability.
| Original language | English |
|---|---|
| Pages (from-to) | 73-85 |
| Number of pages | 13 |
| Journal | Archives of Thermodynamics |
| Volume | 37 |
| Issue number | 1 |
| DOIs | |
| Publication status | Published - 1 Mar 2016 |
UN SDGs
This output contributes to the following UN Sustainable Development Goals (SDGs)
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SDG 13 Climate Action
Keywords
- Membrane air separation
- Oxygen production
ASJC Scopus subject areas
- General Physics and Astronomy
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